CN112237945B - Preparation and application of noble metal cluster catalyst for acetylene hydrochlorination - Google Patents
Preparation and application of noble metal cluster catalyst for acetylene hydrochlorination Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 50
- 229910000510 noble metal Inorganic materials 0.000 title claims abstract description 49
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 title claims description 20
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 title claims description 17
- 238000002360 preparation method Methods 0.000 title claims description 12
- 238000007038 hydrochlorination reaction Methods 0.000 title description 10
- 229910052736 halogen Inorganic materials 0.000 claims abstract description 5
- 150000002367 halogens Chemical class 0.000 claims abstract description 5
- 125000000962 organic group Chemical group 0.000 claims abstract description 5
- 239000013110 organic ligand Substances 0.000 claims abstract description 5
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract 2
- 239000011574 phosphorus Substances 0.000 claims abstract 2
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 44
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 27
- 238000003756 stirring Methods 0.000 claims description 24
- 238000006243 chemical reaction Methods 0.000 claims description 22
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 19
- 239000003960 organic solvent Substances 0.000 claims description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 18
- QBVXKDJEZKEASM-UHFFFAOYSA-M tetraoctylammonium bromide Chemical group [Br-].CCCCCCCC[N+](CCCCCCCC)(CCCCCCCC)CCCCCCCC QBVXKDJEZKEASM-UHFFFAOYSA-M 0.000 claims description 13
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 12
- 238000001035 drying Methods 0.000 claims description 12
- 229910052737 gold Inorganic materials 0.000 claims description 11
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical group CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 10
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 9
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical group ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 claims description 9
- 239000002243 precursor Substances 0.000 claims description 9
- 238000005406 washing Methods 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 8
- 239000012279 sodium borohydride Substances 0.000 claims description 7
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 7
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 6
- 125000004429 atom Chemical group 0.000 claims description 6
- 239000003638 chemical reducing agent Substances 0.000 claims description 6
- 239000004094 surface-active agent Substances 0.000 claims description 6
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 claims description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- 230000002194 synthesizing effect Effects 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 229910052697 platinum Inorganic materials 0.000 claims description 3
- 229910052794 bromium Inorganic materials 0.000 claims description 2
- 229910052801 chlorine Inorganic materials 0.000 claims description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims description 2
- 229910052740 iodine Inorganic materials 0.000 claims description 2
- -1 monohexanethiol Chemical compound 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 claims description 2
- 239000001509 sodium citrate Substances 0.000 claims description 2
- XTEGARKTQYYJKE-UHFFFAOYSA-M Chlorate Chemical group [O-]Cl(=O)=O XTEGARKTQYYJKE-UHFFFAOYSA-M 0.000 claims 2
- RFCQDOVPMUSZMN-UHFFFAOYSA-N 2-Naphthalenethiol Chemical compound C1=CC=CC2=CC(S)=CC=C21 RFCQDOVPMUSZMN-UHFFFAOYSA-N 0.000 claims 1
- ADJJLNODXLXTIH-UHFFFAOYSA-N adamantane-1-thiol Chemical compound C1C(C2)CC3CC2CC1(S)C3 ADJJLNODXLXTIH-UHFFFAOYSA-N 0.000 claims 1
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 abstract description 5
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 abstract description 4
- ORILYTVJVMAKLC-UHFFFAOYSA-N adamantane Chemical compound C1C(C2)CC3CC1CC2C3 ORILYTVJVMAKLC-UHFFFAOYSA-N 0.000 abstract description 4
- ZMRFRBHYXOQLDK-UHFFFAOYSA-N 2-phenylethanethiol Chemical compound SCCC1=CC=CC=C1 ZMRFRBHYXOQLDK-UHFFFAOYSA-N 0.000 abstract description 2
- 239000010931 gold Substances 0.000 description 40
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 8
- 230000003197 catalytic effect Effects 0.000 description 7
- 229910004042 HAuCl4 Inorganic materials 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 5
- 239000004800 polyvinyl chloride Substances 0.000 description 5
- 229920000915 polyvinyl chloride Polymers 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- FFRBMBIXVSCUFS-UHFFFAOYSA-N 2,4-dinitro-1-naphthol Chemical compound C1=CC=C2C(O)=C([N+]([O-])=O)C=C([N+]([O-])=O)C2=C1 FFRBMBIXVSCUFS-UHFFFAOYSA-N 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002105 nanoparticle Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000004627 transmission electron microscopy Methods 0.000 description 3
- 229910002621 H2PtCl6 Inorganic materials 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 239000002082 metal nanoparticle Substances 0.000 description 2
- 238000002186 photoelectron spectrum Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 229910052723 transition metal Inorganic materials 0.000 description 2
- 150000003624 transition metals Chemical class 0.000 description 2
- 239000005997 Calcium carbide Substances 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- QZPSXPBJTPJTSZ-UHFFFAOYSA-N aqua regia Chemical compound Cl.O[N+]([O-])=O QZPSXPBJTPJTSZ-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- XTEGARKTQYYJKE-UHFFFAOYSA-N chloric acid Chemical group OCl(=O)=O XTEGARKTQYYJKE-UHFFFAOYSA-N 0.000 description 1
- 229940005991 chloric acid Drugs 0.000 description 1
- RCTYPNKXASFOBE-UHFFFAOYSA-M chloromercury Chemical compound [Hg]Cl RCTYPNKXASFOBE-UHFFFAOYSA-M 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012776 electronic material Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010574 gas phase reaction Methods 0.000 description 1
- 150000002343 gold Chemical class 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000002198 insoluble material Substances 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000005309 metal halides Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 125000004437 phosphorous atom Chemical group 0.000 description 1
- 238000001420 photoelectron spectroscopy Methods 0.000 description 1
- 239000003223 protective agent Substances 0.000 description 1
- 238000013139 quantization Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 238000005556 structure-activity relationship Methods 0.000 description 1
- 125000004434 sulfur atom Chemical group 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/226—Sulfur, e.g. thiocarbamates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/48—Silver or gold
- B01J23/52—Gold
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/189—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms containing both nitrogen and phosphorus as complexing atoms, including e.g. phosphino moieties, in one at least bidentate or bridging ligand
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/20—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
- B01J35/23—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/391—Physical properties of the active metal ingredient
- B01J35/393—Metal or metal oxide crystallite size
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/07—Preparation of halogenated hydrocarbons by addition of hydrogen halides
- C07C17/08—Preparation of halogenated hydrocarbons by addition of hydrogen halides to unsaturated hydrocarbons
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/30—Addition reactions at carbon centres, i.e. to either C-C or C-X multiple bonds
- B01J2231/32—Addition reactions to C=C or C-C triple bonds
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- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
- B01J2531/0213—Complexes without C-metal linkages
- B01J2531/0222—Metal clusters, i.e. complexes comprising 3 to about 1000 metal atoms with metal-metal bonds to provide one or more all-metal (M)n rings, e.g. Rh4(CO)12
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- B01J2531/18—Gold
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Abstract
The invention provides a noble metal atom cluster and a catalyst, wherein the atom cluster is a noble metal atom cluster structure protected by an organic ligand, and the structural formula is An(SR)mOr An(PB)mCxA is a noble metal, B is an organic group coordinated with phosphorus (P), and C is a halogen; SR is at least one of phenethyl mercaptan, 2-naphthalene mercaptan, monohexanethiol or adamantane mercaptan, n is 2-200, m is 10-200, and x is 2-20.
Description
Technical Field
The invention relates to a supported noble metal cluster catalyst for synthesizing vinyl chloride through acetylene hydrochlorination, and a preparation method and application thereof, belonging to the field of catalyst preparation technology and application in organic synthesis.
Background
Vinyl chloride, abbreviated as VCM, is a monomer for the synthesis of polyvinyl chloride (PVC). PVC is one of five general resins (PVC, PE, PP, PS and ABS) in the world, has good physical and mechanical properties, and is used for producing building, packaging and electronic materials. With the rapid development of world economy, the living standard of people is continuously improved, and the demand of PVC materials is increased year by year. Currently, there are 3 main methods for industrial production of vinyl chloride: the acetylene method, the ethylene method and the ethane method are countries with less petroleum reserves and relatively rich coal resources in China, so the calcium carbide method becomes a main method for PVC production in China. The preparation of vinyl chloride by reaction of acetylene with vinyl chloride is carried out in a gas phase reaction in the presence of a heterogeneous solid catalyst based on mercury chloride on a fixed bed. However, due to the toxicity of Hg, there has been an increasing search for mercury-free catalysts, such as noble metal halides, transition metals, and the like. However, the service life of these catalysts is far below that of mercury-based compounds.
As early as eighties of the twentieth century, teaching g.j. hutchings in the united kingdom suggested that trivalent gold supported on activated carbon could efficiently catalyze the hydrochlorination of acetylene. In this report, it is pointed out that the active component is Au3+,Au3+Is obtained by impregnating a carrier with a precursor of the metal in the presence of an oxidizing agent such as aqua regia. However, the investigators found that 0-valent gold was also catalytically active. For example, chinese patent CN104707602A discloses a catalyst in which Au in an oxidized state is supported on activated carbon, protected with PVA, preferably in a size between 2nm and 6 nm. Chinese patent CN104549522A discloses a catalyst containing noble metals Pd, Pt and Au as active components, S2-、S2O3 2-、SO3 2-The non-mercury catalyst of the allelic promoter catalyzes the hydrochlorination of acetylene. This is an example of a noble metal nanoparticle as a catalyst for the hydrochlorination of acetylene.
The traditional nanoparticle catalyst has polydispersity, which adds great difficulty to the apparent catalytic activity and thus the intrinsic structure. To overcome these difficulties, clusters having high dispersibility and high stability, especially clusters having precise numbers of atoms, are important. Compared to nanoparticles (>2nm), clusters (<2nm) possess some unique properties: (1) the space structure is adjustable: nanogold generally exists in a face-centered cubic structure, and a gold atomic cluster spatial structure is significantly influenced by size and atomic number; (2) electronic energy band quantization: the electron bands of nanogold are generally continuously distributed, while the electron bands of gold clusters are generally discontinuously and quantitively distributed.
Disclosure of Invention
The invention aims to provide a novel acetylene hydrochlorination catalyst. The invention discloses a method for catalyzing acetylene hydrochlorination by using noble metal clusters with specific sizes and specific atomic numbers, which is based on the fact that the structure-activity relationship is difficult to establish when nano particles are used for catalyzing acetylene hydrochlorination.
The purpose of the invention is realized by the following modes:
the invention provides a noble metal atomic cluster which is protected by an organic ligand and has a structural formula An(SR)mOr An(PB)mCxA is a noble metal, B is an organic group coordinated with P, C is halogen, SR is one or more of phenethyl mercaptan, 2-naphthalene mercaptan, monohexanethiol and adamantane mercaptan, n is 2-200, n represents the number of noble metal atoms, m is 10-200, m represents the number of organic ligands, x is 2-20, and x represents the number of halogen atoms.
Based on the technical scheme, the noble metal atom cluster is preferably Au or Pt. Halogen is Br, Cl, I; organic group coordinated to P is Ph3Or Ph2Py is used. The particle size of the noble metal cluster catalyst is less than 2 nm.
Based on the technical scheme, the noble metal preferably has the valence of delta + and delta of 0-1.
The invention also provides a supported noble metal cluster catalyst, wherein the supported noble metal cluster catalyst is obtained by supporting the noble metal cluster on a carrier, and the supporting amount is 0.5-2%.
Based on the technical scheme, the carrier is preferably acid-treated modified activated carbon.
The invention also provides a preparation method of the noble metal cluster catalyst, which specifically comprises the following experimental steps:
mixing a noble metal precursor with an organic solvent A, adding a surfactant, stirring for 15-60min, adding an organic ligand, stirring for 1-3 hours, adding a reducing agent, stirring for reaction for 3-20 hours at 20-50 ℃, washing with an organic solvent B, dissolving with an organic solvent C to remove insoluble substances, volatilizing the organic solvent C, and drying to obtain the noble metal cluster catalyst; the molar weight of the surfactant is 1-3 times of that of the noble metal precursor, and the molar weight of the reducing agent is 5-20 times of that of the noble metal precursor.
The invention also provides a preparation method of the supported noble metal cluster catalyst, which comprises the steps of stirring 5-15% hydrochloric acid at normal temperature for 24 hours to obtain modified activated carbon, dispersing the activated carbon in an organic solvent D to obtain a solution A, and dispersing the noble metal cluster catalyst in the solvent D according to claim 1 to obtain a solution B; the organic solvent D is dichloromethane; and mixing the solution A and the solution B, stirring for 3-12h at 20-50 ℃, centrifuging, washing and drying to obtain the catalyst.
Based on the above technical scheme, preferably, the noble metal precursor is chloric acid of a corresponding metal.
Based on the technical scheme, preferably, the surfactant is tetraoctyl ammonium bromide (TOAB) or hexadecyl trimethyl ammonium bromide (CTAB); the reducing agent is sodium borohydride, sodium citrate and glycol; the organic solvent A is Tetrahydrofuran (THF), methanol and ethanol; the organic solvent B is methanol, n-hexane or ethanol; the organic solvent C is dichloromethane, acetonitrile or acetone.
Based on the technical scheme, the catalyst is preferably applied to the reaction for synthesizing vinyl chloride by hydrochlorination of acetylene, the reaction temperature is 150-250 ℃, and the reaction raw materials are HCl and C2H2(ii) a The HCl and C2H2The molar ratio of (1-2: 1) and the space velocity of 0.2-0.8ml g-1min-1。
Advantageous effects
(1) The noble metal cluster catalyst researched by the invention has the advantages of simple and feasible synthesis method and high yield.
(2) The noble metal cluster catalyst researched by the invention uses high-activity noble metal as an active component, avoids the insufficient activity of transition metal, and meets the requirement of industrial application.
(3) Compared with the common noble metal nano-particles, the noble metal atomic cluster researched by the invention has uniform size.
(4) According to the noble metal cluster catalyst, the protective agent is mercaptan and triphenylphosphine (diphenyl-2-pyridylphosphine), and S and P atoms can better stabilize the cluster and prevent the cluster from agglomerating.
(5) The noble metal cluster catalyst researched by the invention has the advantages of excellent stability, environmental protection, recycling and operability of industrial application.
Drawings
FIG. 1 is Au prepared in example 125AC Transmission Electron Microscopy (TEM).
FIG. 2 is Au prepared in example 211AC Transmission Electron Microscopy (TEM).
FIG. 3 is Au prepared in example 3144AC Transmission Electron Microscopy (TEM).
FIG. 4 is a photoelectron spectrum (XPS) of three catalysts in example 4.
Figure 5 is a graph of the selectivity and conversion of the catalyst in example 5.
Figure 6 is a graph of the selectivity and conversion of the catalyst in example 6.
FIG. 7 is a graph of the selectivity and conversion of the catalyst in example 7.
Detailed Description
The invention is further described in detail below with reference to the drawings and the detailed description.
Example 1
Au25(PhC2H4S)18Preparation of the/AC catalyst
60mg of HAuCl were weighed4·4H2O into a 50mL three-necked flask, 15mL THF was added and the solution was golden yellow. TOAB 92mg (TOAB: HAuCl) was added4·4H21.16mol of O: 1mol) of goldThe yellow color slowly deepens to orange-red. Stirring for 30min, adding PhCH2CH2SH 97μL(PhCH2CH2SH:HAuCl4·4H2O is 5 mol: 1mol), stirring for one hour at 25 ℃, and adding NaBH4(4mL of iced water) 55mg (NaBH)4:HAuCl4·4H2O is 10 mol: 1 mol). The reaction was stopped by stirring for three hours. Washing the product with n-hexane and methanol, dissolving the precipitate with dichloromethane, removing insoluble substances, and drying to obtain Au25(PhC2H4S)18。
Dispersing the hydrochloric acid treated active carbon with dichloromethane, and dropwise adding Au dissolved in dichloromethane25(PhC2H4S)18Stirring overnight at 25 ℃, and centrifugally drying to obtain Au25/AC。
Au prepared as in example 1 is shown in FIG. 125AC transmission electron microscope picture, the diameter of the gold particle is about 1.3 nm.
Example 2
Au11(PPh2Py)7Br3Preparation of the/AC catalyst
240mgHAuCl was weighed4And 306mgPPh2Py, add 0.0105mL H2O, the solvent is ethanol, stirring is carried out for 9.5h at the temperature of 25 ℃, and the Au is obtained after the ethanol washing and dryingI(PPh2Py) Cl. Weigh 40mg of [ Au ]I(PPh2Py)Cl]And 85mg of tetra-n-octylammonium bromide (TOAB: HAuCl)4·4H21.16mol of O: 1mol) was dissolved in 10mL of ethanol and stirred in a round-bottomed flask (600rpm/min), followed by the addition of NaBH4(15.2mg,NaBH4:HAuCl4·4H2O is 5 mol: 1mol) was dissolved in 1mL of ethanol and slowly added dropwise. After 12h of reaction, the mixture was poured into 10mL of water, centrifuged through a 4000rpm centrifuge to give a black solid, washed several times with n-hexane/dichloromethane (v/v-5/1) to remove excess PPh2Py ligand and TOAB. Finally, the precipitate obtained above was extracted with 2mL of methanol, centrifuged again (10000rpm, 5min) to remove insoluble material, and the resulting solution was dried by a rotary evaporator to obtain Au11(PPh2Py)7Br3。
Dispersing the hydrochloric acid treated active carbon with dichloromethane, and dropwise adding Au dissolved in dichloromethane11(PPh2Py)7Br3Stirring overnight at 25 ℃, and centrifugally drying to obtain Au11/AC。
Au prepared as in example 1 is shown in FIG. 211AC transmission electron microscope picture, the diameter of the gold particle is about 1.2 nm.
Example 3
Au144(C6H13S)60Preparation of the/AC catalyst
60mg of HAuCl were weighed4·4H2O into a 50mL three-necked flask, 15mL of methanol was added and the solution was golden yellow. TOAB 92mg (TOAB: HAuCl) was added4·4H21.16mol of O: 1mol), the solution slowly deepens from golden yellow to orange red. Stirring for 30min, adding C6H13SH 87μL(C6H13SH:HAuCl4·4H2O is 5 mol: 1mol), stirring for one hour at the normal temperature of 25 ℃, and adding NaBH4(4mL of iced water) 55mg (NaBH)4:HAuCl4·4H2O is 10 mol: 1 mol). The reaction was stopped by stirring at 25 ℃ for five hours. Washing the product with methanol, washing with acetone, dissolving the precipitate with dichloromethane, removing insoluble substances, and drying to obtain Au144(C6H13S)60。
Dispersing the hydrochloric acid treated active carbon with dichloromethane, and dropwise adding Au dissolved in dichloromethane144(C6H13S)60Stirring overnight at 25 ℃, and centrifugally drying to obtain Au144/AC。
Au prepared as shown in FIG. 3 for example 3144AC transmission electron microscope picture, the diameter of the gold particle is about 1.9 nm.
Example 4
Pt-PhC2H4Preparation of SH/AC catalysts
133.3mg of H are weighed2PtCl6·6H2O into a 50mL three-necked flask, 15mL THF was added and the solution was yellow. TOAB 281.6mg (TOAB: H) was added2PtCl6·6H2O is 2 mol: 1 mol). Stirring for 30minAdding PhCH2CH2SH35.6μL(PhCH2CH2SH:H2PtCl6·6H2O is 1 mol: 1mol), stirring for one hour at 25 ℃, and adding NaBH4(4mL of iced water) 146mg (NaBH)4:H2PtCl6·6H2O15 mol: 1 mol). The reaction was stopped by stirring for eight hours. Washing the product with n-hexane and methanol, dissolving the precipitate with dichloromethane, removing insoluble substances, and drying to obtain Pt-PhC2H4SH。
Dispersing the hydrochloric acid treated active carbon with dichloromethane, and dropwise adding Pt-PhC dissolved in dichloromethane2H4SH, stirring overnight at 25 ℃, and centrifugally drying to obtain Pt-PhC2H4SH/AC。
Example 5
The oxidation state of the catalysts in examples 1, 2, 3 was characterized by photoelectron spectroscopy.
XPS samples were prepared by tableting 50mg of the catalyst of examples 1, 2 and 3.
FIG. 4 is a photoelectron spectrum of three catalysts, from which gold 4f can be seen7/2In Au0(83.8eV) and Au+(85.4eV), the valence of gold is delta +, and delta is 0-1.
Example 6
Au25(SR)18The catalytic activity of the/AC catalyst.
1g of the catalyst of example 1 was loaded in a fixed bed reactor having an internal diameter of 8mm at a space velocity of 0.6ml g- 1min-1,HCl:C2H2Reaction at 180 ℃ for 48h, 1.09. The initial conversion of acetylene was 88.5%, the selectivity was 100% and there was no decrease over 48 h.
As shown in FIG. 5, is Au25(SR)18The catalytic activity of the/AC catalyst.
Example 7
Au11The catalytic activity of the/AC catalyst.
1g of the catalyst of example 2 was loaded in a fixed bed reactor having an internal diameter of 8mm at a space velocity of 0.6ml g- 1min-1,HCl:C2H2=1.09, at 180 ℃ for 48 h. The initial conversion of acetylene was 89.4%, the selectivity was 100% and there was no decrease over 48 h.
As shown in FIG. 6, is Au11The catalytic activity of the/AC catalyst.
Example 8
Au144(SR)60The catalytic activity of the/AC catalyst.
1g of the catalyst of example 3 was loaded in a fixed bed reactor having an internal diameter of 8mm at a space velocity of 0.6mlg-1min-1,HCl:C2H2Reaction at 180 ℃ for 48h, 1.09. The initial conversion of acetylene was 89.7%, the selectivity was 100% and there was no decrease over 48 h.
As shown in FIG. 7, is Au144(SR)60The catalytic activity of the/AC catalyst.
Claims (6)
1. The application of the supported noble metal cluster catalyst is characterized in that the catalyst is applied to the reaction of synthesizing chloroethylene by hydrochlorinating acetylene, the noble metal cluster is supported on a carrier, and the supported amount is 0.5-2%; the carrier is acid-treated modified activated carbon; the structural formula of the noble metal atom cluster is A n (SR) m Or A n (PB) m C x A is a noble metal, B is an organic group coordinated with phosphorus (P), and C is a halogen; SR is SC2H4At least one of Ph, 2-naphthalene thiol, monohexanethiol, or adamantanethiol,n=2-200,m=10-200,x= 2-20; the noble metal is Au or Pt; wherein the valence of the noble metal is delta +, and delta is 0-1; the organic group coordinated to P is Ph3Or Ph2Py;
The preparation method of the noble metal atom cluster comprises the following steps:
mixing a noble metal precursor with an organic solvent A, adding a surfactant, stirring for 15-60min, adding an organic ligand, stirring for 1-3 hours, adding a reducing agent, stirring at normal temperature for reaction for 3-20 hours, washing with an organic solvent B, dissolving with an organic solvent C to remove insoluble substances, volatilizing the organic solvent C, and drying to obtain the noble metal cluster; the molar weight of the surfactant is 1-3 times that of the noble metal precursor, and the molar weight of the reducing agent is 5-20 times that of the noble metal precursor;
the organic solvent A is Tetrahydrofuran (THF), methanol and ethanol; the organic solvent B is methanol, n-hexane or ethanol; the organic solvent C is dichloromethane, acetonitrile or acetone.
2. Use according to claim 1, wherein the halogen is Br, Cl, I; the particle size of the noble metal cluster is less than 2 nm.
3. The use according to claim 1, wherein the supported noble metal cluster catalyst is prepared by a process comprising the steps of:
(1) stirring the activated carbon with hydrochloric acid with the concentration of 5-15% at 20-50 ℃ for 24h to obtain acid-treated modified activated carbon, dispersing the activated carbon in an organic solvent D to obtain a solution A, and dispersing the noble metal atom clusters in the organic solvent D to obtain a solution B; the organic solvent D is dichloromethane;
(2) and mixing the solution A and the solution B, stirring for 3-12h at 20-50 ℃, centrifuging, washing and drying to obtain the catalyst.
4. Use according to claim 1, wherein the noble metal precursor is a chlorate of the corresponding metal.
5. Use according to claim 1, wherein the surfactant is tetraoctylammonium bromide (TOAB), cetyltrimethylammonium bromide (CTAB); the reducing agent is sodium borohydride, sodium citrate and glycol.
6. The application of claim 1, wherein the reaction temperature in the reaction for synthesizing vinyl chloride by hydrochlorinating acetylene is 150 ℃ and 250 ℃, and the reaction raw materials are HCl and C2H2(ii) a The HCl and C2H2In a molar ratio of1-2:1, space velocity of 0.2-0.8mL g-1 min-1。
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